ahmed alterkait · 2019. 12. 10. · knpc efforts towards reducing hydrocarbon loss & flare gas...

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  • AHMED ALTERKAIT Snr Eng, Manufacturing Excellence - KNPC

  • KNPC EFFORTS TOWARDS REDUCING HYDROCARBON LOSS & FLARE GAS MANAGEMENT Introduction. Challenges Efforts Made: Review the measurement methodology :

    losses type, Source , measurement & breakdown Defining the uncertainties. reconciliation method & Correction factors

    Conclusion

  • Introduction KNPC Operates highly complex Refineries.

    Complex units & integration Thousands of valves flowmeters & analyzers More than 20 Elevated Flare Stacks

    Current Capacity over 700,000 BPD

  • Challenges In 2015, High hydrocarbon loss (by balance) reported.

    Refinery Loss ( loss by balance) = Refinery input – Refinery output – Fuels + (∆ Inventory).

    The same was captured by SAB & raised in the

    parliament.

  • Efforts Made committee formed to review accounting methodologies

    & practices being followed. Defining the losses type, Source breakdown,

    accounting Methodologies Defining the uncertainty reasons. Defining the correction factors

  • Finding :

    Loss Types: Controllable loss : Losses that can be reduced to the bench mark levels based on the

    refinery configuration.

    Non-Controllable loss : Losses that is part of normal refinery operation ( i.e. side

    products or side loss )

  • Finding:

    Controllable Losses

    Breakdown Measurement Method Reference

    H/c loss through Flares (Ex H2) 13% Flowmeters Chevron feedback , International Standards

    H/c loss to Bio-treatment

    6%

    Analysis + Calculation Newly Identified, IP Document Page 34

    H/C in Sea Water effluent Analysis + Calculation Record Available , to be reported

    API Evaporation & Process Fugitives Analysis + Calculation Records available, to be re-classified and reported as per the standards. IP Document Page 8

    Hydrogen Venting Flowmeters Record Available. To be included in loss report for MAA & MAB

  • Finding:

    Non-controllable Process Losses Breakdown Measurement Method Reference

    Carbon loss as CO2 from HP Units 71% Mass Balance, part of production International Standard IP Doc Page 34 & Solomon Methodology

    H2 loss as H2O from SRU Units

    10%

    Mass Balance, part of production

    International Standard, IP Doc page 7 Record available to be reported.

    Nitrogen Loss as NH3 Mass Balance, part of

    production

    International Standard IP Doc Page 34 No record for MAA & SHU.

    FCC Coke Heat Balance Solomon Methodology

    CCR Coke Heat Balance Newly Identified found in IP Document page 7

    Flare Pilot & Purge Design figures Solomon Methodology

    VOC Emissions analysis & calculations Solomon Methodology Hydrocarbon in dispatched Ash (WWT) / waste

    analysis Newly Identified, found in IP document Page 9

  • Defining the uncertainty reasons Instrumentation errors

    Test run to ensure instrumentation accuracy. Systematic error. Random error.

    Non-hydrocarbon interference. Analyze the flared gas and deduct the purge gas

    quantities and the non hydrocarbon gases. Zero value losses

    Part of the refinery operation.

  • Reconciliation method & Obtaining Correction factors • Reconciliation method link

  • ۱۳

    Compressor Suction K.O.D

    Drain

    Passing PSV

    Compressor Stuffing Box

    Lines

    Passing Control Valves

    GT Passing Gas Traps

    Flare header FG Purge

    Passing Sample Point Purge

    Passing v/v of De-Pressurizing lines

    Passing pump casing vent

  • Reconciliation method & Obtaining Correction factors • Obtaining Correction factors

    Lab analysis. Field survey. Link Mass Balance.

  • AccuTrack – a small hand-held device that measures the sound created by gases or liquids passing through an opening. V-Pac – a much more sophisticated device to measure sound. Can estimate quantity of passing. IR Camera – Multi-purpose tool that projects real-time picture showing temperature gradients.

    http://home.knpc.net/../temp/VALVECP.AVI

  • Conclusion

    81% of the refinery reported loss found to be zero value, wherein 71% due to CO2 venting from HPU.

    Max Unaccountable Loss for MAA = 0.7% & MAB = 0.5%

    Totally new sources of losses have been identified.

    71

    ۱۰%

    ۱۳% ٦%

    ۱۹%

    LOSS BY BALANCE BREAKDOWNS CO2 Other uncontrollables Flaring Other Controllables

  • Conclusion • H/C Loss Book Value reduced by 81 % • Improvement in physical HC Loss reported by Solomon since 2014 study.

    KNPC are within the international companies practices. < 1%

    KNPC reached the boundary for the first quartile for 2018 Solomon study

    with hc loss of about 0.2X%.

  • THANK YOU

    Slide Number 1Slide Number 2Slide Number 3KNPC EFFORTS TOWARDS REDUCING HYDROCARBON LOSS & FLARE GAS MANAGEMENTIntroductionChallengesEfforts MadeFinding : �Finding:�Finding: �Defining the uncertainty reasonsReconciliation method & Obtaining Correction factorsSlide Number 13Slide Number 14Reconciliation method & Obtaining Correction factorsSlide Number 16ConclusionConclusionSlide Number 19